• 대한기계학회논문집B
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• 제28권12호
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• pp.1535-1548
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• 2004

Condensation heat transfer experiments were conducted with the oblong shell and plate heat exchanger without oil in a refrigerant loop using R-l34a, R-407C and R-410A. An experimental refrigerant loop has been developed to measure the condensation heat transfer coefficient h$_{r}$ and frictional pressure drop $\Delta$p$_{f}$ of the various refrigerants in a vertical oblong shell and plate heat exchanger. The effects of the refrigerant mass flux(40∼80kg/$m^2$s), average heat flux(4∼8kW/$m^2$), refrigerant saturation temperature(30∼4$0^{\circ}C$) and vapor quality of refrigerants on the measured data were explored in detail. Similar to the case of a plate heat exchanger, even at a very low Reynolds number, the flow in the oblong shell and plate heat exchanger remains turbulent. A comparison of the performance of the various refrigerants revealed that R-410A had the highest heat transfer performance followed by R-l34a, and R-407C had the lowest performance of the refrigerants tested. The pressure drops were also reported in this paper. The pressure drops for R-410A were approximately 45% lower than those of R-l34a. R-407C had 30% lower pressure drops than R-l34a. Experimental results were compared with several correlations which predicted condensation heat transfer coefficients and frictional pressure drops. Comparison with the experimental data showed that the previously proposed correlations gave unsatisfactory results. Based on the present data, empirical correlations of the condensation heat transfer coefficient and the friction factor were proposed.tor were proposed.sed.

• 설비공학논문집
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• 제7권1호
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• pp.63-72
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• 1995

Convective heat transfer in a two-dimensional horizontal and vertical channel with isothermal rectangular beams attached to one adiabatic wall is investigated from the numerical solution of Navier-Stokes and energy equations. The solutions have been obtained for dimensionless beam spacings, S/L=1~4, aspect ratios of beam, H/B=0.25~4, Reynolds numbers, Re=50~1000 and Grashof numbers, $Gr=0{\sim}5{\times}10^4$. The total mean Nusselt number, Nu_T for horizontal and vertical channels shows same value at Gr=0. As Gr increases, Nu_T for horizontal channel increases, but Nu_T for vertical channel shows similar value at S/L=2, H/B=0.25, Re=100. The total mean Nusselt number for horizontal channel is higher than that for vertical channel. As H/B increases, $Nu_T$ for both channel decrease at $Gr=10^4$, Re=100.

• 대한기계학회논문집B
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• 제29권7호
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• pp.854-860
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• 2005

Pool boiling heat transfer characteristics of R-134a were investigated in titanium plain and low finned tubes. The diameter of test tube was 15.88 mm and the fin density was 33 fpi. Tests were conducted at saturation temperatures of $20^{\circ}C$ and $30^{\circ}C$. Heat fluxes varied from 5000 W/$m^2$ to 50,000 W/$m^2$ based on surface area of the plain tube. The pool boiling heat transfer coefficients of the titanium horizontal plain tube are lower than those of the copper plain tube by $8.2\%$. The boiling heat transfer coefficients of the low finned tube are averagely higher than those of the plain tubes by $34\%$. The average deviation of the Slipcevic correlation from the present data for the low finned tube is $20\%$.

• 대한기계학회논문집B
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• 제39권10호
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• pp.817-824
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• 2015

본 논문은 수직 오리피스 노즐의 유동 및 물질전달 특성에 대한 실험적 연구를 목적으로 한다. 구동유체 및 부유체의 유량, 용존산소 농도 그리고 소비 전력을 측정하였으며, 고속 카메라를 이용한 직접 촬영 기법으로 수직 혼합유동의 가시화 이미지를 획득하였다. 측정자료를 이용하여 질량비, 총괄 산소전달 계수 그리고 물질전달 성능계수를 도출하였다. 구동압력이 증가하면 질량비는 약간 감소하는 반면에, 산소전달 계수와 소비전력은 증가하였다. 구동압력이 증가하고 질량비가 작아지면, 기포의 미세화가 촉진되고 확산도가 증대되기 때문에 산소 전달율이 증가하였다.

• 한국안광학회지
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• 제8권1호
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• pp.59-64
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• 2003

Photochoromic lens에 광을 조사하면 darkening 상태와 fading상태에서photo-transmittance는 감소한다. 광의 조사를 제거하면 fading 상태가 되어 photo-transmittance는 원래 상태로 회복하는 가역과정을 갖는다. 자체 제작한 Photochoromic lens에서 darkening과 fading 과정에서 Photochromism의 분광측색계를 이용하여 CIE $L^*a^*b^*$의 색 좌표을 얻는다. darkening과 fading상태에서 색 좌표($a^*-b^*$)는 일차 곡선이고 (-) 기울기를 이며, 선형적으로 변한다. 색 좌표 이동량은 Blue ${\rightarrow}$ Yellow, Red ${\rightarrow}$ Green형태이다. fading상태에서 색 좌표는 darkening 상태보다 $b^*$ 값이 낮고, Photochromism 좌표의 이동은 darkening 상태와 반대로 이동한다. Photochoromic lens에 대한 Photochoromism 평가 방법은 darkening과 fading에 대한 색 좌표 이동으로 이용 할 수 있다.

• 대한기계학회논문집B
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• 제24권2호
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• pp.233-240
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• 2000

An experimental study of condensation heat transfer was performed for pure refrigerants HFC32, HFCI25, and HFC134a, and a ternary refrigerant mixture of HFC32/125/134a (23/25/52wt%). The heat transfer coefficients were measured inside a horizontal smooth tube 5.8 mm I.D. and 8.0 m long. The refrigerant temperature at inlet was 40 $^{\circ}C$, and the mass flux was varied from 150 to 400 $kg/m^2s$. As for the pure refrigerants, the heat transfer coefficient of HFC32/125/l34a decreased as the quality decreased. In addition, the heat transfer coefficient of HFC32/l25/134a was about 20 % lower than HFC 134a at a low mass flux but showed no reduction at a high mass flux. The heat transfer coefficient of ternary refrigerant mixtures was 30% lower on the average than that of the pure refrigerant.

• 대한기계학회논문집B
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• 제39권1호
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• pp.61-69
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• 2015

본 논문은 수직 오리피스 이젝터의 혼합유동 및 산소전달 특성에 대한 실험적 연구를 목적으로 한다. 실험장치는 전동 모터-펌프, 오리피스 이젝터, 순환 수조, 공기압축기, 고속 카메라 시스템 그리고 제어 및 측정기기로 구성하였다. 측정된 구동유체 및 유입공기의 유량을 이용하여 유량비를 도출하였다. 이적터에서 분출된 혼합유동의 가시화를 통해 정성적 거동을 고찰하였으며, 용존산소 농도를 측정하여 총괄 산소전달계수를 도출하였다. 구동유체의 유량이 일정하고 압축기의 공기압이 높아지면 유량비와 산소전달계수는 증가하며, 압축기의 공기압이 일정하고 구동유체의 유량이 증가하면 유량비는 감소하지만 산소전달계수는 증가하였다. 기포의 크기에 따른 체류시간 및 확산도와 수직 혼합유동의 도달거리는 2 상의 접촉면적과 시간에 크게 영향을 미치기 때문에 산소전달율의 중요한 변수임을 유추할 수 있다.

• 대한기계학회논문집B
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• 제26권2호
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• pp.318-327
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• 2002

In this paper, heat transfer and pressure oscillation characteristics on oscillating capillary tube heat pipe(OCHP) according to input heat flux, mixture ratio of working fluid and inclination angle were investigated and were compared single working fluid(R-142b) with binary mixture working fluid(R-142b-Ethano1). OCHP was made to serpentine structure of loop type with 10 turns by drilling the channels of length 220mm, width 1.5mm, and depth 1.5mm on the surface of brass plate. In this study, R-l42b and R-l42b-Ethanol were used as working fluids, the charging ratio of working fluids was 40(vol.%), the input heat flux to evaporating section was changed from 0.3W/㎠ to 1.8W/㎠, and mixture ratio of working fluid was R(100%), R(95%)-E(5%), R(90%)-E(10%), and R(85%)-E(15%). From the experimental results, it was found that the effective thermal conductivity of single working fluid was better than that of binary mixture working fluid. But, in case of binary mixture working fluid, critical heat flux was higher than that of single working fluid. And, the higher the mixture ratios of working fluid, the lower heat transfer performance. In case of pressure oscillation, as the inclination angle was lower, pressure wave was more irregular. These phenomena were more serious when the working fluid was binary mixture. Besides, when mixture ratio was higher, saturated pressure was increased, more irregular wave was observed and the mean amplitude was increased. For the same input heat flux, inclination angle and charging ratio, when pressure oscillation has sinusoidal wave, mean amplitude was small, and saturated pressure was low value, the heat transfer was excellent.

• 대한기계학회논문집B
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• 제37권9호
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• pp.815-821
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• 2013

고분자 전해질 연료전지(이하 PEMFC) 시스템의 효율과 수명은 유입되는 공기의 습도에 직접적인 영향을 받는다. 그러므로 공기는 정상 운전조건에서 적절한 습도를 유지시켜 주어야 한다. 하지만 가습 장치의 특성들에 대해서는 연구가 부족한 상태이다. 본 연구에서는 정상상태에서 다양한 입구조건에 따른 막 가습기의 수분전달 특성을 알아보기 위해 실험을 수행하였다. 실험에 이용할 평판형 막 가습기를 제작하였으며, 실험에 적합한 환경을 조성하였다. 우선 일정한 온도 조건하에서 막을 통과하는 수분 전달 능력을 실험하였고 이후 다양한 입구 조건에 따른 수분 전달 특성을 알아보았다. 본 실험에서 사용된 입구조건의 변수는 건공기와 습공기의 유량, 작동온도, 작동압력 및 유동배열이 있으며 각각의 입구 조건이 가습기의 성능에 미치는 영향을 논의하였다.

• 멤브레인
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• 제18권3호
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• pp.219-225
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• 2008

본 연구에서는 atom transfer radical polymerization (ATRP)에 의해 polydimethylsiloxane (PDMS)와 methyl-methacrylate (MMA)로부터 polydimethylsiloxane-polymethylmethacrylate (PDMS-PMMA) block copolymer를 합성하였다. 합성된 PDMS-b-PMMA copolymer막의 특성은 FT-IR, $^1H$ NMR, GPC, DSC 등을 사용하여 조사하였다. 질소와 수소의 투과도는 각각 $1.2{\sim}l.5$ barrer와 $6.2{\sim}10.5$ barrer를 보였고, 질소에 대한 수소의 선택도는 $5.3{\sim}6.9$ 범위였다. PDMS-b-PMMA copolymer 막의 투과도와 선택도는 PDMS 막보다는 낮은 값을 보였고, PMMA 막보다는 높은 결과를 보였다.